Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
  • C08L67/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds

Definitions

• This invention relates to thermoformed articles such as trays and a method for improving their preparation and handling properties.
• U.S. Patent 4,380,621 discloses a fast crystallizing polyester in which at least some of the end groups of the polyester have the formula --Y ⁇ M+, where M+ is an alkaline metal ion, preferably sodium.
• the compositions can be prepared by polymerizing the polyester in the presence of an alkaline metal salt or corresponding base, such as NaOH.
• the composition can be compounded with various additives, including an oxidized polyethylene wax containing carboxylic acid groups.
• the composition is useful preparing molding powder for use in preparing injection molded articles.
• U.S. Patent 4,801,640 discloses a polyester film with improved dimensional stability, abrasion resistance, drawability, and slip properties.
• the film contains hardened organic particles such as melamine/formaldehyde resin and a nucleating agent selected from various alkali metal salts, including salts of ester waxes.
• U.S. Patent 4,365,036 discloses fast crystallizing polyalkyleneterephthalate resins containing a crystallization promoter which is a complex of sodium iodide and a polymeric compound, together with fillers or additives including paraffin. The product is useful as a molded composition.
• U.S. Patent 4,448,913 discloses polyethylene terephthalate molding compositions characterized by rapid crystallization, provided by combining PET and a filler or reinforcing agent with a crystallization rate promoter comprising sodium benzoate and a poly-alpha-olefin such as low density polyethylene. Examples of the composition include small amounts of wax.
• thermoformed articles such as trays from thermoplastic, crystallizable polyester, a polymeric crack stopping agent such as poly-4-methylpentene-1, and a nucleating agent such as talc.
• U.S. Patent 4,463,121 discloses walled thermoformed articles of partially crystallized polyethylene terephthalate containing a minor component of a polyolefin which exhibit improved impact resistance.
• Traditional nucleating agents such as talc are not required.
• Japanese publication 57/025352 discloses a polyester resin composition with improved mold release property, comprising glass fiber, a metal chelate such as sodium acetylacetone chelate, montan wax, and PET resin.
• the composition has excellent moldability, mold release property, and luster.
• Japanese publication 59/109551 discloses a dimensionally stable polyester resin composition prepared by adding montan wax ester to glass fiber reinforced PET. Good mold release properties are imparted.
• Japanese publication 57/096,039 discloses a polybutylene terephthalate resin composition including ammonium polyphosphate and paraffin.
• the resin composition has good mechanical properties and external appearance.
• Japanese publication 55/154,130 discloses a slidable polyester film containing micropowdered silica coated with polyolefin wax. The blend is extruded into a sheet which is then stretched.
• Japanese publication 56/109,245 discloses a polyethylene terephthalate resin composition containing e.g. polyethylene wax.
• a crystal nucleating agent such as sodium benzoate or stearate, etc., may be present.
• the composition exhibits a glossy appearance even when molded in a low temperature metallic mold.
• Japanese publication 53/143,651 discloses rotary articles obtained by blending polybutylene terephthalate resin with a wax which is solid at ordinary temperatures.
• Plastic trays suitable for oven use have become increasingly popular in recent years.
• a commonly used plastic for making such trays is crystalline polyethylene terephthalate (CPET), since it provides good high temperature properties and can withstand cooking at e.g. 200°C or above for 0.5 hours or longer.
• CPET compositions include crystallization promoters such as low density polyethylene in levels of up to several percent, to provide rapid crystallization for ease of processing.
• the use of such blends of polymers have certain disadvantages.
• polymeric blends are generally less readily recyclable than are compositions consisting of substantially a single polymer.
• PET compositions containing other polymers can present processing difficulties.
• PET pellets almost always need to be dried at high temperature before melt processing.
• Pellets of polyethylene cannot withstand high temperatures without melting.
• formed articles which contain a significant amount of polyethylene cannot be readily prepared from a "single bag" mixture of pellets of PET and the polyethylene.
• polyethylene in such blends can lead to deposits on casting rolls and vacuum forming equipment.
• the present invention provides articles made from CPET which retain processability and rapid crystallization without addition of polyethylene.
• thermoformed articles such as trays, prepared from a blend consisting essentially of
• the invention further provides a process for preparation of a thermoformed article, comprising the steps of
• Thermoformed articles of the present invention are made from a blend comprising mostly a thermoplastic, crystallizable polyester resin.
• Suitable polyester resins include certain polyalkylene terepthalates, polyethylene 2,6-naphthalenedicarboxylate, poly-1,4-di(methylene)cyclohexane terephthalate, and especially polyethylene terephthalate (PET).
• PET is a well known material, prepared by a condensation polymerization process to provide a polymer of alternating units derivable from ethylene glycol and terephthalic acid.
• Small amounts of other comonomers derivable from such entities as isophthalic acid or cyclohexane dimethanol may be incorporated to change the melting point or crystallization rate of the polymer; a branching agent, such as trimethylolpropane, pentaerythritol, or a comonomer derivable from a benzene tricarboxylic acid such as trimellitic acid, may be incorporated to provide for improved melt strength. Polymers with improved melt strength are more easily cast into flat sheet which does not "neck in” as it exits the die.
• the amount of PET in the composition used to form the articles may be for example about 90 to about 99.9 percent by weight and is preferably about 99 to about 99.8 percent by weight.
• sodium ion sufficient to function as an effective crystallization agent to permit an efficient thermoforming process to be carried out.
• This sodium ion will normally be present as a counterion in association with carboxylate end groups on the polymer chain derived from terephthalic acid moieties.
• the sodium ions can be added as a sodium-PET component, that is, sodium neutralized PET.
• sodium neutralized PET is a known material, the preparation of which is described in U.S. patent 4,830,621, the disclosure of which is incorporated herein by reference.
• sodium ions can be added in any other form which will form sodium-PET in situ, provided that the added anion will not exhibit any deleterious effects.
• a suitable sodium ionomer can be used as the sodium source.
• Sodium salts of fatty acids are less desirable, since their presence may lead to reduction of the molecular weight of the polymer.
• the amount of sodium ion which is present should normally be about 60 to about 250 parts per million, based on the PET. If less than about 60 parts per million are present the improved rate of crystallization will not be fully realized, whereas at above about 250 parts per million the crystallization rate would likely be too fast, making it difficult to cast amorphous sheet. Furthermore, the presence of excessive amounts of sodium ions may have a detrimental effect on the molecular weight of the polymer. Preferably the amount of sodium ion is about 100 to about 250 parts per million. If the sodium ion is supplied in the form of sodium-PET, the amount of sodium-PET required will of course vary with the number of neutralized acid end groups on the PET.
• an appropriate level of sodium can be supplied by addition of about 3 to about 15 percent by weight of a concentrate of PET resin containing about 800 to about 4500 parts per million sodium ion. Preferably about 5 to about 10 percent of sodium-PET containing about 1500 to about 2000 parts per million sodium ion can be used.
• the wax preferably should be substantially free from reactive groups or other moieties which would lower the intrinsic viscosity of the polyester matrix to such an extent that the resulting trays become brittle.
• Suitable waxes thus include polyolefin waxes such as polypropylene wax or polyethylene wax, preferably oxidized high density polyethylene wax and, especially, low density polyethylene wax. Waxes which may be less suitable include paraffin wax, amide waxes, metallic soaps, and glycols.
• waxes may provide some of the advantages of the present invention if the intrinsic viscosity of the starting polyester is sufficiently high that embrittlement is not a problem. It is also desirable, for trays to be used for food, that the wax have necessary governmental approvals for such use.
• the wax can be supplied to the composition separately if desired, but more conveniently it is supplied as a concentrate of PET resin containing about 2 to about 11 percent wax. (Above levels of about 9 weight percent, the composition becomes difficult to melt blend.)
• This concentrate if desired, can be the same concentrate which supplies the sodium ion, described above.
• Traditional amounts of other additives, such as antioxidants, fillers, whiteners such as titanium dioxide, colorants such as channel black or phthalocyanine, and processing aids can also be added to the composition, either separately or by way of a concentrate.
• the components are melt blended together by customary means using equipment such as blenders or extruders. After blending, the polymeric mixture is normally extruded into a sheet by techniques well known to those skilled in the art of thermoforming polyethylene terephthalate. In particular, the molten sheet should be quenched promptly after it emerges from the die, in order to ensure that the PET of the sheet is in a substantially amorphous state.
• the articles of the present invention are finally prepared by subjecting the sheet to thermoforming.
• the sheet can be converted to a heat stable shape by any thermoforming method, such as vacuum assist, air assist, mechanical plug assist or matched mold thermoforming.
• Thermoforming methods such as these are well known to those skilled in the art, and normally include preheating of the sheet to above its glass transition temperature, in order to promote formability.
• the thermoforming mold itself should be heated to a temperature sufficient to allow the sheet to be shaped and permit the initially amorphous PET to crystallize to some extent, e.g., 25-35%.
• the operable range of mold temperatures is about 120 to 215°C, with a preferred range of about 130 to 190°C.
• Examples of articles that can be prepared using thermoforming processes are containers such as bottles, jars, cans, bowls, trays, and dishes.
• the formed part can be stripped out of the thermoforming mold cavity by known means. Once the heat-set part has been removed from the mold, the excess portion of the sheeting which remains attached to the part is trimmed away. The remainder of the material (regrind) can be reintroduced into the extruder and recycled as desired.
• thermoforming step and subsequent processing steps reveal themselves in the thermoforming step and subsequent processing steps.
• the presence of the sodium ion provides for suitably rapid crystallization of the PET at the thermoforming temperatures, so that the initially amorphous material is at least partially crystallized within the length of time it is retained within the thermoforming mold.
• the presence of the wax provides freedom from formation of feathered edges upon trimming away of the excess portion of the sheeting and also minimizes problems with denesting or sticking of items such as trays, when they are stacked.
• the thermoformed parts further have good appearance and color properties.
• Cube blends were prepared of components A and B, as indicated in the following Table.
• Component A was polyethylene terephthalate resin containing about 0.2 weight percent copolymerized trimellitic acid branching agent, intrinsic viscosity 1.05, except as noted.
• Component B was either a single component or a precompounded blend of the components as indicated in the Table.
• the major constituent of Component B was either linear low density polyethylene (LLDPE) or sodium PET, i.e., the same PET as described above but containing 1770 ppm sodium and having an inherent viscosity of 0.70.
• LLDPE linear low density polyethylene
• Other materials present in component B in some of the examples included a wax, either oxidized high density polyethylene wax, 0.95 g/cm3, m.p.
• Composition % by weight A B C1 100 --none--- -- -- -- C2 97 LLDPE 3 -- -- -- C3 92.5 NaPET 7.5 -- -- -- 1 92 NaPET 7.5 PED521 0.3 TiO2 0.2 Irg 0.02 2 92 NaPET 7.5 PE 520 0.3 TiO2 0.2 Irg 0.02 C4 97 a LLDPE 3 -- -- -- a. PET, IV 0.95, from Goodyear.
• the cube blends were dried and extruded into amorphous sheets. Certain of the sheets, 0.76 mm (30 mils) thick, were thermoformed into crystallized trays.
• a comparative thermoforming run was started by adjusting the conditions for commercial material (Comparative Example C4) to give best forming results and then varying cycle time for a control (Comparative Example C1) and a sheet containing sodium containing PET as the only additive (Comparative Example C3).
• the oven heaters were set at 421°C and mold temperature at 177°C. Forming times for optimum performance were as shown in Table II: Table II Example Cycle Time, seconds C4 5.7 to 7.0 C1 10.7 to 12 C3 6.0 to 6.6
• thermoforming rate of the PET/NaPET blend matches the commercial CPET control (C4) which is a blend with polyethylene.
• C3 the trays without polyethylene (C3) were observed to cut poorly on the tray trimming press, generating hairs and feathered edges, making them commercially unacceptable.
• the cut trays when stacked also exhibited a sticking or denesting problem which would make them unacceptable.
• CPET trays from the wax-containing blend of Example 1 were prepared as described above. Trays from this composition were observed to cut without generating hairs or feathered edges and did not exhibit a denesting problem.

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• Chemical & Material Sciences (AREA)
• Health & Medical Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
• Compositions Of Macromolecular Compounds (AREA)
• Manufacture Of Macromolecular Shaped Articles (AREA)
• Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

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• 1990
  • 1990-12-04 US US07/622,420 patent/US5102943A/en not_active Expired - Lifetime
• 1992
  • 1992-01-16 AU AU10259/92A patent/AU643864B2/en not_active Ceased
  • 1992-01-17 CA CA002059614A patent/CA2059614A1/en not_active Abandoned
  • 1992-01-20 EP EP92300478A patent/EP0552520A1/de not_active Withdrawn
  • 1992-01-21 JP JP4029040A patent/JPH0662788B2/ja not_active Expired - Fee Related

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